EP3384078B1 - Procédé de fabrication de non-tissé présentant des propriétés de surface améliorées - Google Patents

Procédé de fabrication de non-tissé présentant des propriétés de surface améliorées Download PDF

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Publication number
EP3384078B1
EP3384078B1 EP15802111.3A EP15802111A EP3384078B1 EP 3384078 B1 EP3384078 B1 EP 3384078B1 EP 15802111 A EP15802111 A EP 15802111A EP 3384078 B1 EP3384078 B1 EP 3384078B1
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Prior art keywords
fibres
aqueous suspension
process according
web
surfactant
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German (de)
English (en)
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EP3384078A1 (fr
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Mikael Strandqvist
Hannu Ahoniemi
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Essity Hygiene and Health AB
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Essity Hygiene and Health AB
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    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/42Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
    • D04H1/4374Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece using different kinds of webs, e.g. by layering webs
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/42Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
    • D04H1/4266Natural fibres not provided for in group D04H1/425
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/44Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling
    • D04H1/46Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres
    • D04H1/465Hydraulic needling
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/44Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling
    • D04H1/46Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres
    • D04H1/492Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres by fluid jet
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/44Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling
    • D04H1/46Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres
    • D04H1/498Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres entanglement of layered webs
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/10Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between yarns or filaments made mechanically
    • D04H3/105Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between yarns or filaments made mechanically by needling
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H5/00Non woven fabrics formed of mixtures of relatively short fibres and yarns or like filamentary material of substantial length
    • D04H5/02Non woven fabrics formed of mixtures of relatively short fibres and yarns or like filamentary material of substantial length strengthened or consolidated by mechanical methods, e.g. needling
    • D04H5/03Non woven fabrics formed of mixtures of relatively short fibres and yarns or like filamentary material of substantial length strengthened or consolidated by mechanical methods, e.g. needling by fluid jet
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/002Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines by using a foamed suspension
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/22Agents rendering paper porous, absorbent or bulky
    • D21H21/24Surfactants
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/50Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by form
    • D21H21/56Foam
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H27/00Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/002Tissue paper; Absorbent paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H27/00Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/30Multi-ply
    • D21H27/32Multi-ply with materials applied between the sheets
    • D21H27/34Continuous materials, e.g. filaments, sheets, nets
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H27/00Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/30Multi-ply
    • D21H27/32Multi-ply with materials applied between the sheets
    • D21H27/34Continuous materials, e.g. filaments, sheets, nets
    • D21H27/36Films made from synthetic macromolecular compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H5/00Special paper or cardboard not otherwise provided for
    • D21H5/26Special paper or cardboard manufactured by dry method; Apparatus or processes for forming webs by dry method from mainly short-fibre or particle material, e.g. paper pulp
    • D21H5/2678Manufacture of layered products (assembly of superposed sheets), comprising the consolidation of such a structure
    • D21H5/2685Manufacture of layered products (assembly of superposed sheets), comprising the consolidation of such a structure by dry method on to a web or on or between several preformed webs, at least one of which has been formed by another method, e.g. by wet method

Definitions

  • the present invention relates to a process for producing a fibre-containing nonwoven sheet material having a minimum of surface irregularities and to a sheet material which is obtainable by such a process.
  • Absorbent nonwoven materials are used for wiping various types of spills and dirt in industrial, medical, office and household applications. They typically comprise a combination of thermoplastic polymers (synthetic fibres) and cellulosic pulp for absorbing both water and other hydrophilic substances, and hydrophobic substances (oils, fats).
  • the nonwoven wipes of this type in addition to having sufficient absorptive power, are at the same time strong, flexible and soft. They can be produced by wet-laying a pulp-containing mixture on a polymer web, followed by dewatering and hydroentangling to anchor the pulp onto the polymer and final drying. Absorbent nonwoven materials of this type and their production processes are disclosed in WO2005/042819 .
  • WO99/22059 discloses a method of producing a nonwoven sheet material by providing melt-blown or spun-laid synthetic continuous filaments to form a polymer layer, applying a foam of natural (pulp) fibres on a side thereof through a head box to produce a combination of synthetic filaments and natural fibres, followed by hydroentangling the combination using water jets, to produce a composite sheet material in which the filaments and the natural fibres are intimately integrated resulting in high strength and high stiffness sheet material.
  • the hydroentanglement can be preceded by applying the foam also on the other side of the polymer layer.
  • WO03/040469 teaches a similar process in which part of the starting materials is directly introduced into the head box, i.e. separate from the foam.
  • WO2012/150902 discloses a method of producing a hydroentangled nonwoven material wherein a first fibrous web of synthetic staple fibres and natural (pulp) fibres is wet-laid and hydroentangled, spun-laid filaments are laid on top of the hydroentangled first fibrous web and a second fibrous web of natural fibres is wet-laid on top of the filaments and subsequently hydroentangled. The web is then reversed and subjected to a third hydroentangling treatment at the side of the first fibrous web, to produce a strong composite sheet material having essentially identical front and back sides.
  • Desirable results in terms of flexibility, sheet strength and absorption capacity are obtained when the pulp-containing web is produced by applying the pulp in the form of a foam containing a surfactant, onto or together with a synthetic polymer, and bonding the combined pulp fibres and synthetic polymer by hydroentanglement.
  • surface irregularities or even thin spots or holes in the final sheet material may result, which negatively affect the sheet properties and performances as well as its appearance.
  • This problem could be reduced by using relatively high levels of surfactant in the foam-forming pulp mixture, but high levels of surfactant turn out to hamper the hydroentangling process.
  • high levels of surfactant may hamper the water purification in the recycling loop of water used in the hydroentangling, which in turn may interfere with the hydroentangling of the nonwoven material and hence result in suboptimum bonding in the nonwoven product.
  • the object of the invention is to provide a hydroentangled, absorbent fibre-containing nonwoven material having reduced surface irregularities and limited levels of surfactants, in combination with high strength resulting from effective bonding through hydroentanglement.
  • a further object is to provide a process for producing such nonwoven materials which involves multiple steps of wet-laying a fibre-containing suspension prior to hydroentanglement.
  • the invention pertains to a process of producing hydroentangled nonwoven materials as defined in appended claim 1.
  • the invention furthermore pertains to hydroentangled nonwoven materials obtainable by such a process as defined in appended claim 12 and to a hygiene article as defined in appended claim 15.
  • the present process of producing a hydroentangled nonwoven sheet material comprises the following steps:
  • steps b) and c) are repeated at least once, wherein any repeating deposition of aqueous suspension containing short fibres and a surfactant is applied on a surface of the fibrous web of short fibres that has been previously formed.
  • the composition of the aqueous suspension to be used in steps b) and b') and optional further steps b") may be different or the same, but is preferably essentially the same.
  • the dry solids content of the fibrous web after step c) and before step b') is preferably at least 15 wt.%, more preferably between 20 and 40 wt.%, and even more preferably between 25 and 30 wt.%.
  • aqueous suspension to be applied in steps b) and b') may be the same or different. For example, between 25 and 75 wt.% of the aqueous suspension (on dry solids basis) can be applied in step b), between 15 and 60 wt.% of the aqueous suspension can be applied in step b'), and between 0 and 40 wt.% of the aqueous suspension can be applied in one or more optional further steps b") following step c').
  • the short fibres may comprise natural fibres and/or synthetic fibres and may in particular have average lengths between 1 and 25 mm.
  • Part or all of the natural short fibres may comprise cellulosic pulp preferably having fibre lengths of between 1 and 5 mm.
  • the cellulosic (pulp) fibres may constitute at least 25 wt.%, preferably 40-95 wt.%, more preferably 50-90 wt.%, of the short fibres to be provided in step a).
  • the short fibres may comprise man-made staple fibres having fibre lengths of between 5 and 25 mm, preferably between 6 and 18 mm.
  • the staple fibres may constitute at least 3 wt.%, preferably 5-50 wt.% of the short fibres to be provided in step a).
  • the aqueous suspension preferably contains the short fibres at a level of between 1 and 25 wt.%.
  • the suspension preferably contains between 0.01 and 0.1 wt.% of a non-ionic surfactant.
  • the aqueous suspension is applied as a foam containing between 10 and 90 vol.% of air.
  • the present process includes the step of providing a polymer web on the carrier prior to step b), onto which the aqueous suspension can be deposited in multiple steps.
  • the polymer web may be formed by a spun-laid, air-laid or carding process step.
  • the polymer web preferably contains at least 50 wt.% of synthetic filaments.
  • the present process includes an optional step of depositing a polymer layer on the deposited (combined) fibrous web after steps b) and c), and preferably after step c').
  • aqueous suspension is deposited at the same side in steps b) and b'), while optional further depositions in steps b") may be at the same or opposite sides.
  • hydroentanglement of step d) is preferably performed only from one side.
  • the nonwoven material as produced may have front and back surfaces of different composition.
  • a carrier on which the aqueous composition can be applied can be a forming fabric, which can be a running belt-like wire having at least the breadth of the sheet material to be produced, which fabric allows draining of liquid through the fabric.
  • a polymer web can first be deposited on the carrier by laying man-made fibres on the carrier.
  • the fibres can be short or long distinct (staple) fibres and/or continuous filaments. The use or co-use of filaments is preferred.
  • a polymer layer can be deposited on the fibrous web obtained in steps b) and c), preferably after step c') or even after step c"), but before step d). It is also possible to first deposit a polymer layer, followed by depositing the aqueous suspension to form a fibrous web on the polymer web and to deposit a further polymer layer on the fibrous web.
  • Filaments are fibres that in proportion to their diameter are very long, in principle endless, during their production. They can be produced by melting and extruding a thermoplastic polymer through fine nozzles, followed by cooling, preferably using an air flow, and solidification into strands that can be treated by drawing, stretching or crimping.
  • the filaments may be of a thermoplastic material having sufficient coherent properties to allow melting, drawing and stretching.
  • useful synthetic polymers are polyolefins, such as polyethylene and polypropylene, polyamides such as nylon-6, polyesters such as poly(ethylene terephthalate) and polylactides. Copolymers of these polymers may of course also be used, as well as natural polymers with thermoplastic properties.
  • Polypropylene is a particularly suitable thermoplastic man-made fibre. Fibre diameters can e.g. be in the order of 1-25 ⁇ m. Staple fibres can be of the same man-made materials as filaments, e.g. polyethylene, polypropylene, polyamides, polyesters, polylactides, cellulosic fibres, and can have lengths of e.g. 2-40 mm.
  • the polymer web contains at least 50 wt.% of thermoplastic (synthetic) filaments, more preferably at least 75 wt.% of synthetic filaments.
  • the combined web contains between 15 and 45 wt.% of the synthetic filaments on dry solids basis of the combined web.
  • the aqueous suspension is obtained by mixing short fibres and water in a mixing tank.
  • the short fibres can comprise natural fibres, in particular cellulosic fibres.
  • suitable cellulosic fibres are seed or hair fibres, e g cotton, flax, and pulp.
  • Wood pulp fibres are especially well suited, and both softwood fibres and hardwood fibres are suitable, and also recycled fibres can be used.
  • the pulp fibre lengths can vary between 0.5 and 5, in particular from 1 to 4 mm, from around 3 mm for softwood fibres to around 1.2 mm for hardwood fibres and a mix of these lengths, and even shorter, for recycled fibres.
  • the pulp can be introduced as such, i.e. as pre-produced pulp, e.g. supplied in sheet form, or produced in situ, in which case the mixing tank is commonly referred to as a pulper, which involves using high shear and possibly pulping chemicals, such as acid or alkali.
  • Staple (man-made) fibres of variable length, e.g. 5-25 mm, can suitably be used as additional fibres.
  • the stable fibres can be man-made fibres as described above, e.g. polyolefins, polyesters, polyamides, poly(lactic acid), or cellulose derivatives such as lyocell.
  • the staple fibres can be colourless, or coloured as desired, and can modify further properties of the pulp-containing suspension and of the final sheet product.
  • Levels of additional (man-made) fibres, in particular staple fibres can suitably be between 3 and 50 wt.%, preferably between 5 and 30 wt.%, more preferably between 7 and 25 wt.%, most preferably between 8 and 20 wt.% on the basis of the dry solids of the aqueous suspension.
  • Suitable surfactants include anionic, cationic, non-ionic and amphoteric surfactants.
  • anionic surfactants include long-chain (Ic) (i.e. having an alkyl chain of at least 8 carbon atoms, in particular at least 12 carbon atoms) fatty acid salts, Ic alkyl sulfates, Ic alkylbenzenesulfonates, which are optionally ethoxylated.
  • Examples of cationic surfactants include Ic alkyl ammonium salts.
  • non-ionic surfactants include ethoxylated Ic fatty alcohols, ethoxylated Ic alkyl amides, Ic alkyl glycosides, Ic fatty acid amides, mono- and diglycerides etc..
  • amphoteric (zwitterionic) surfactants include Ic alkylammonio-alkanesulfonates and choline-based or phosphatidylamine-based surfactants.
  • the level of surfactant (on the basis of the aqueous suspension) can be between 0.005 and 0.2, preferably between 0.01 and 0.1, most preferably between 0.02 and 0.08 wt.%.
  • the amount of air introduced into the suspension can be between 5 and 95 vol.% of the final suspension (including the air), preferably between 15 and 80 vol.%, most preferably between 20 and 60 vol.% or even between 20 and 40 vol.%.
  • the more air is present in the foam often the higher levels of surfactants are required.
  • air is to be interpreted broadly as any non-noxious gas, typically containing at least 50% of molecular nitrogen, and further varying levels of molecular oxygen, carbon dioxide, noble gases etc. Further information about foam formation as such can be found e.g. in WO03/040469 .
  • the aqueous suspension containing short fibres is deposited on the carrier, either directly or on a polymer web, e.g. using a head box, which guides and spreads the suspension evenly over the width of the carrier or the web in the direction of the running fabric, causing the suspension to partly penetrate into the polymer web.
  • the speed of application of the aqueous suspension which is the running speed of the fabric (wire) and thus typically the same as the speed of laying the polymer web, can be high, e.g. between 1 and 8 m/sec (60-480 m/min), especially between 3 and 5 m/sec.
  • the total amount of liquid circulated by the wet-laying or foam laying can be in the order of 50-125 I/sec (3-7.5 m 3 /min), especially 75-110 I/sec (4.5-6.6 m 3 /min).
  • aqueous fibre-containing suspension such as a pulp containing suspension is applied onto the polymer web in at least two separate steps at the same side of the polymer web, using two head boxes.
  • the two (or more) steps are only separated by a suction step c). This results in part of the solids of the suspension entering on and in the polymer web as a result of the deposition and subsequent (or virtually simultaneous) removal of surplus water and air, and consequently the remaining part(s) of the suspended solids to be even more evenly spread over the width of the web.
  • the water content of the combined web before the second pulp application step is preferably not more than 85 wt.%, more preferably not more than 80 wt.%, in particular between 60 and 75 wt.%.
  • the dry solids content of the fibrous web after the first application step is preferably at least 15 wt.%, more preferably between 20 and 40 wt.%, and even more preferably between 25 and 40 wt.% or even between 25 and 30 wt.%.
  • the second (and optional further) steps are also followed (or effectively accompanied) by a suction step c).
  • the relative amounts of suspension (or of solids) applied in the first and second (and possibly third and further) steps can be equal. However it was found to be preferable to apply the suspension at slightly decreasing levels. Thus, between 25 and 75 wt.% of the aqueous suspension (on dry solids basis) can be applied in a first step, between 15 and 60 wt.% of the aqueous suspension can be applied in a second step, and between 0 and 40 wt.% of the aqueous suspension can be applied in an optional third or further step. In an example, between 50 and 70 wt. of the suspension is applied in the first step and between 30 and 50 wt.% is applied in the second step.
  • between 40 and 60 wt.% is applied in the first step, between 20 and 40 wt.% is applied in the second step and between 15 and 35 wt.% is applied in a third step.
  • an amount of 40-100 I/sec can be applied in the first step and 15-60 I/sec can be applied in a second step (on water basis).
  • the composition of the fibre-containing suspensions in the first head box (first application) and second head box - and optional further head boxes - is preferably the same. However, if desired, the composition may also be different. For example the ratio of pulp to staple fibres may be different, or the staple fibres may be absent in one of the deposition steps, for example the second deposition step b'), or the staple fibres may be different in length or in other properties such as colour. Alternatively, the level of air - and hence of surfactant - may be different, e.g. lower in the second or further application.
  • the combined web is subjected to hydro-entanglement, i.e. to needle-like water jets covering the width of the running web. It is preferred to perform the hydroentangling step (or steps) on a different carrier (running wire), which is more dense (smaller sieve openings) than the carrier on which the fibre-containing suspensions (and optionally first the polymer web) are deposited. It is further preferred to have multiple hydroentanglement jets shortly sequencing each other.
  • the pressure applied may be in the order of 20-200 bar.
  • the total energy supply in the hydroentangling may step be in the order of 100-400 kWh per ton of the treated material, measured and calculated as described in CA 841938 , pages 11-12.
  • the skilled person is aware of further technical details of hydro-entanglement, as described e.g. in CA 841938 and WO96/02701 .
  • the combined, hydroentangled web is preferably dried, e.g. using further suction and/or oven drying at temperatures above 100°C, such as between 110 and 150°C.
  • the dried nonwoven can be further treated by adding additives, e.g. for enhanced strength, scent, printing, colouring, patterning, impregnating, wetting, cutting, folding, rolling, etc. as determined by the final use of the sheet material, such as in industry, medical care, household applications.
  • additives e.g. for enhanced strength, scent, printing, colouring, patterning, impregnating, wetting, cutting, folding, rolling, etc. as determined by the final use of the sheet material, such as in industry, medical care, household applications.
  • the nonwoven sheet material as produced can have any shape, but frequently it will have the form of rectangular sheets of between less than 0,5 m up to several meters. Suitable examples include wipes of 40 cm x 40 cm. Depending on the intended use, it may have various thicknesses of e.g. between 100 and 2000 ⁇ m, in particular from 250 to 1000 ⁇ m.
  • the sheet material has improved surface evenness, in particular reduced variations in thickness or basis weight per surface area unit, as compared to a similar material formed by a process known in the art, e.g. a similar process using only one head box for applying a pulp-containing material on a polymer.
  • the difference in basis weight (in g/m 2 ) between any two spots of a defined surface area is less than 15%, preferably less than 10%.
  • the sheet material may be essentially homogenous, or it may gradually change from relatively pulp-rich at one surface to relatively pulp-depleted at the opposite surface (as a result of e.g. wet-laying or foam-laying pulp at one side of the polymer web only), or, alternatively, from relatively pulp-rich at both surfaces to relatively pulp-depleted in the centre (as a result of e.g. wet-laying or foam-laying pulp at both sides of the polymer web - either or both in multiple steps at the same side).
  • the nonwoven material as produced has front and back surfaces of different composition, in that the pulp-containing suspension is applied at the same side in each separate step, and/or hydroentanglement is performed only at one side.
  • Other structures are equally feasible, including structures not containing filaments.
  • the sheet material may contain between 25 and 85 wt.% of (cellulosic) pulp, and between 15 and 75 wt.% of man-made (non-cellulosic) polymer material, whether as (semi)continuous filaments or as relatively short (staple) fibres, or both.
  • the sheet material may contain between 40 and 80 wt.% of pulp, between 10 and 60 wt.% of filaments and between 0 and 50 wt.% of staple fibres, or, even more preferred between 50 and 75 wt.% of pulp, between 15 and 45 wt.% of filaments and between 3 and 15 wt.% of staple fibres.
  • the nonwoven sheet material has few if any deficiencies combined with low residual levels of surfactant.
  • the end product contains less than 75 ppm of the surfactant, preferably less than 50 ppm, most preferably less than 25 ppm of (water-soluble) surfactant.
  • thermoplastic polymer is fed into a heated drawing device 1 to produce filaments 2, which are deposited on a first running wire 3 to form a polymer layer.
  • a mixing tank 4 has inlets for pulp 5, staple fibre 6, water 7 and/or 18, air 8, and surfactant (not shown).
  • the resulting pulp-containing suspension (foam) 9 is divided into flows 14 and 15, through controllable valve 13, which flows are fed to the first head box 10 and second head box 16, respectively, which deposit the fibre mass 11 and 17, respectively, on one side of the polymer layer.
  • Suction boxes 12 below the moving wire remove most of the liquid (and gaseous) residue of the spent pulp-containing suspension, and the resulting aqueous liquid is returned to the mixing tank through line 18.
  • the combined pulp-polymer web 19 is transferred to a second running wire 20 and subjected to multiple hydroentanglement steps through devices 21 producing water jets 22, with water suction boxes 23, the water being discharged and further recycled (not shown).
  • the hydroentangled web 24 is then dried in drier 25 and the dried web 26 is further processed (not shown).
  • the even formation of the sheet was assessed by scanning A4-sized nonwoven specimens (290x200 mm), one layer at a time with black backgrounds (consisting of 3 thick black A4 sheets), in a flatbed scanner (Epson Perfection V750 PRO). The images were then converted to grey scale pictures (Grey scale 8 with 8 bit) having 1496x2204 pixels resolution using Image Pro 6.2 software (Media Cybernetics, Bethesda, MD, USA). Good formation is defined as having nonwoven fibres equally distributed in the sheet with as few thin and open areas present as possible. Pixel clusters being equal to or larger than 15 pixels and having a grey scale value below 160 are considered as formation defects in this method and are seen in the sheet either as thin areas, that can be visually seen through, or as holes.
  • a formation value is calculated by adding the pixel count (number of individual pixels) of continuous pixel clusters being larger than 15 pixels and having grey scale values below 160 and dividing by the total number of available pixels.
  • the formation number is essentially the relative amount of thin areas and holes to thicker areas with good formation expressed in percentages. Materials with low formation numbers have better formation and thus better fibre distribution than materials with higher numbers.
  • the basis weight (grammage) can be determined by a test method following the principles as set forth in the following standard for determining the basis weight: WSP 130.1.R4 (12) (Standard Test Method for Mass per Unit Area). In the Standard Method, test pieces of 100x100 mm are punched from the sample sheet. Test pieces are chosen randomly from the entire sample and should be free of folds, wrinkles and any other deviating distortions. The pieces are conditioned at 23°C, 50 % RH (Relative Humidity) for at least 4 hours. A pile of ten pieces is weighed on a calibrated balance. The basis weight (grammage) is the weighed mass divided by the total area (0.1 m 2 ), and recorded as mean value with standard deviations.
  • best and worst quality samples are selected from a sample sheet of 2x1.5 m area.
  • the sheet is placed on a dark surface and the five best and five worst areas are marked based on visual inspection, the least transparent (closest to the original colour) and least irregular ones being qualified as "best” and the most transparent (dark) or irregular ones as "worst". All marked areas are punched out as circles of 140 mm diameter of each of the five best and five worst spots.
  • the samples are conditioned and then weighed as described above.
  • the basis weight (in g/m 2 ) is recorded. This method of selecting, conditioning and weighing circular test samples of 140 mm diameter represents the test method for determining the difference in basis weight for different spots of the finished sheet materials of the present disclosure.
  • the thickness of a sheet material as described herein can be determined by a test method following the principles of the Standard Test Method for Nonwoven Thickness according to EDANA, WSP 120.6.R4 (12).
  • An apparatus in accordance with the standard is available from IM TEKNIK AB, Sweden, the apparatus having a Micrometer available from Mitutoyo Corp, Japan (model ID U-1025).
  • the sheet of material to be measured is cut into a piece of 200x200 mm and conditioned (23°C, 50 % RH, ⁇ 4 hours). The measurement should be performed at the same conditions. During measurement the sheet is placed beneath the pressure foot which is then lowered. The thickness value for the sheet is then read after the pressure value is stabilised.
  • the measurement is made by a precision Micrometer, wherein a distance created by a sample between a fixed reference plate and a parallel pressure foot is measured.
  • the measuring area of the pressure foot is 5x5 cm.
  • the pressure applied is 0.5 kPa during the measurement. Five measurements could be performed on different areas of the cut piece to determine the thickness as an average of the five measurements.
  • An absorbent sheet material of nonwoven that may be used as a wipe such as an industrial cleaning cloth was produced by laying a web of polypropylene filaments on a running conveyor fabric and then applying on the polymer web a pulp dispersion containing a 88:12 weight ratio of wood pulp and polyester staple fibres, and 0.01-0.1 wt.% of a non-ionic surfactant (ethoxylated fatty alcohol) by foam forming in a head box, introducing a total of about 30 vol.% of air (on total foam volume).
  • the weight proportion of the polypropylene filaments was 25 wt.% on dry weight basis of the end product. The amounts were chosen so as to arrive at a basis weight of the end product of 55 g/m 2 .
  • the combined fibre web was then subjected to hydroentanglement using multiple water jets at increasing pressures of 40-100 bar providing a total energy supply at the hydroentangling step of about 180 kWh/ton as measured and calculated as described in CA 841938 , pp. 11-12 and subsequently dried.
  • Example 1 was repeated with the only difference that the pulp dispersion was applied in two stages, using two head boxes placed at a distance of about 2 m from each other along the production line.
  • the formation data and basis weight data for five samples at the best and worst sites are presented in Table 1 and Table 2, respectively, under the headings "Double Head Box".
  • Table 1 Formation results (in %)
  • Example 1 Example 2 Single Head Single Head Double Head Double Head Box - worst Box - best Box - worst Box - best 1 1.84 0.22 1.77 0.38 2 0.56 0.12 1.44 0.55 3 4.74 0.25 1.00 0.41 4 5.08 0.10 1.00 0.37 5 4.21 0.18 1.81 0.26 Average 3.29 0.17 1.41 0.40 Std. dev. 1.77 0.06 0.35 0.10
  • Table 1 shows that the formation values of the worst spots decrease significantly when using a two head boxes versus using a single one (average from 3.29 to 1.41 %) and that the standard deviation decreases significantly (for the worst spots). Also the difference between worst and best strongly decreases, when using two head boxes as compared to one.
  • Table 2 Basis weight results (in g / m 2 ) Example 1 Example 2 Single Head Single Head Double Head Double Head Box - worst Box - best Box - worst Box - best 1 51.5 62.1 55.6 58.6 2 57.9 61.9 53.3 59.4 3 47.8 61.9 54.1 58.0 4 46.0 63.0 54.7 61.5 5 49.1 62.8 53.7 59.9 Average 50.5 62.3 54.3 59.5 Std. dev. 4.1 0.5 0.8 1.2
  • Table 2 shows that the basis weight improves significantly for the worst spots and that the difference between worst and best decreases significantly.
  • Example 1 was repeated with the only difference that the amounts were chosen so as to arrive at a basis weight of the end product of 80 g/cm 2 .
  • the formation data for 5 different samples of the nonwoven at the best and worst sites are presented in Table 3 below, under the headings "Single Head Box”, with averages and standard deviations.
  • the basis weight data for the same samples are presented in Table 4 below, under the headings "Single Head Box”, with averages and standard deviations.
  • Example 3 was repeated with the only difference that the pulp dispersion was applied in two stages, using two head boxes placed at a distance of about 2 m from each other along the production line.
  • the formation data and basis weight data for five samples at the best and worst sites are presented in Table 3 and Table 4, respectively, under the headings "Double Head Box".
  • Table 3 Formation results (in %)
  • Example 3 Example 4 Single Head Single Head Double Head Double Head Box - worst Box - best Box - worst Box - best 1 0.28 0.16 0.01 0.00 2 0.39 0.04 0.05 0.06 3 0.44 0.06 0.04 0.01 4 0.12 0.03 0.02 0.10 5 0.25 0.13 0.02 0.02 Average 0.30 0.08 0.03 0.04 Std. dev. 0.11 0.05 0.01 0.04
  • Table 3 shows that the formation values for the worst spots decrease significantly when using two head boxes versus using a single one (average from 0.30 to 0.03) and that the standard deviation decreases significantly (for the worst spots). Also the difference between worst and best spots almost disappears.
  • Table 4 Basis weight results (in g / m 2 ) Example 3 Example 4 Single Head Single Head Double Head Double Head Box - worst Box - best Box - worst Box - best 1 68.5 85.8 70.9 82.4 2 66.5 80.2 73.6 75.7 3 66.4 80.8 71.8 82.2 4 74.3 85.0 75.3 79.9 5 74.8 86.3 74.1 80.5 Average 70.1 83.6 73.1 80.1 Std. dev. 3.7 2.6 1.6 2.4
  • Table 4 indicates that the basis weight improves significantly for the worst spots and that the difference between worst and best decreases significantly.
  • a material produced using two head boxes has better fibre distribution than the material formed using one head box.
  • the material formed using two head boxes is more even than the one formed using one head box.
  • the formation number is essentially the relative amount of thin areas and holes to thicker areas with good formation expressed in percentages. Materials with low formation numbers have better formation and thus better fibre distribution than materials with higher numbers.

Claims (15)

  1. Procédé de production d'un matériau en feuille non tissé hydro-enchevêtré de fibres naturelles et/ou synthétiques, comprenant les étapes consistant à :
    a) fournir une suspension aqueuse contenant des fibres courtes et un tensioactif ;
    b) déposer la suspension aqueuse sur un support,
    c) éliminer des résidus aqueux de la suspension aqueuse déposée à l'étape b) pour former une bande fibreuse, et ensuite
    d) hydro-enchevêtrer la bande fibreuse,
    caractérisé par les étapes consistant à
    b') déposer une suspension aqueuse contenant des fibres courtes et un tensioactif sur la surface de la bande fibreuse formée à l'étape c) du côté ne faisant pas face au support, et
    c') éliminer des résidus aqueux de la suspension aqueuse déposée à l'étape b') pour former une bande fibreuse combinée avant l'étape d).
  2. Procédé selon la revendication 1, dans lequel les fibres courtes ont des longueurs comprises entre 1 et 25 mm.
  3. Procédé selon la revendication 2, dans lequel les fibres courtes comprennent au moins 25 % en poids, de préférence 50 à 90 % en poids de pâte cellulosique ayant des longueurs de fibre comprises entre 1 et 5 mm, et/ou les fibres courtes comprennent au moins 3 % en poids, de préférence 5 à 50 % en poids de fibres discontinues ayant des longueurs de fibres comprises entre 5 et 25 mm, de préférence entre 6 et 18 mm.
  4. Procédé selon l'une quelconque des revendications précédentes, dans lequel la composition de la suspension aqueuse est la même aux étapes b et b').
  5. Procédé selon l'une quelconque des revendications précédentes, dans lequel entre 25 et 75 % en poids de la suspension aqueuse (sur une base de solides secs) sont appliqués à l'étape b), entre 15 et 60 % en poids de la suspension aqueuse sont appliqués à l'étape b'), et entre 0 et 40 % en poids de la suspension aqueuse sont appliqués en une ou plusieurs étapes supplémentaires facultatives b") à l'issue de l'étape c').
  6. Procédé selon l'une quelconque des revendications précédentes, dans lequel la teneur en solides secs de la bande fibreuse après l'étape c) et avant l'étape b') est d'au moins 15 % en poids, de préférence entre 20 et 40 % en poids, de manière plus préférée entre 25 et 30 % en poids.
  7. Procédé selon l'une quelconque des revendications précédentes, dans lequel la suspension aqueuse est appliquée sous la forme d'une mousse contenant entre 10 et 90 % en volume, de préférence entre 20 et 40 % en volume d'air.
  8. Procédé selon l'une quelconque des revendications précédentes, dans lequel la suspension aqueuse contient entre 0,01 et 0,1 % en poids d'un tensioactif non ionique, et le matériau en feuille non tissé contient moins de 75 ppm de tensioactif, de préférence moins de 50 ppm du tensioactif.
  9. Procédé selon l'une quelconque des revendications précédentes, dans lequel, avant l'étape b) et/ou après l'étape c'), une bande de polymère est déposée.
  10. Procédé selon la revendication 9, dans lequel la bande de polymère contient au moins 50 % en poids de filaments synthétiques, et de préférence la bande combinée contient entre 15 et 45 % en poids des filaments synthétiques sur une base de solides secs de la bande combinée.
  11. Procédé selon l'une quelconque des revendications précédentes, dans lequel le matériau non tissé tel que produit a des surfaces avant et arrière de composition différente, en ce sens que l'hydro-enchevêtrement de l'étape d) n'est effectué que sur un côté.
  12. Matériau en feuille non tissé hydro-enchevêtré comprenant des fibres courtes et une bande de polymère pouvant être produite par le procédé de la revendication 9 ou 10, qui présente les caractéristiques suivantes :
    - il a des surfaces avant et arrière de composition différente ;
    - il contient moins de 75 ppm, de préférence moins de 50 ppm de tensioactif ;
    - la différence de grammage (en g/m2) entre deux points quelconques selon la méthode de test décrite dans les exemples est inférieure à 15 %.
  13. Matériau en feuille selon la revendication 12, caractérisé en ce qu'il a une épaisseur comprise entre 250 et 1 000 pm et/ou un grammage compris entre 40 et 80 g/m2.
  14. Matériau en feuille selon la revendication 12 ou 13, qui contient entre 40 et 80 % en poids de fibres cellulosiques, entre 3 et 15 % en poids de fibres discontinues, et entre 15 et 45 % en poids de filaments.
  15. Produit d'hygiène, tel qu'une lingette, comprenant un matériau en feuille dimensionné, conditionné et éventuellement emballé selon l'une quelconque des revendications 12 à 14, ou produit par le procédé selon l'une quelconque des revendications 1 à 11.
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CO2018005716A2 (es) 2018-06-12
CN108291345A (zh) 2018-07-17
CN108291345B (zh) 2021-08-17
ZA201804359B (en) 2019-09-25
NZ743252A (en) 2019-09-27
CA3006600C (fr) 2021-02-23
PL3384078T3 (pl) 2020-05-18
HK1258259A1 (zh) 2019-11-08
ES2774928T3 (es) 2020-07-23
MX2018006562A (es) 2018-08-01
US20180355527A1 (en) 2018-12-13
EP3384078A1 (fr) 2018-10-10
WO2017092791A1 (fr) 2017-06-08
AU2015416199A1 (en) 2018-05-17
DK3384078T3 (da) 2020-02-24
US10435826B2 (en) 2019-10-08
CA3006600A1 (fr) 2017-06-08
RU2700916C1 (ru) 2019-09-23
AU2015416199B2 (en) 2019-09-19

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